• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验

两种经验性气液传质测定方法在搅拌罐生物反应器中表征甲烷生物降解的系统比较。

A systematic comparison of two empirical gas-liquid mass transfer determination methodologies to characterize methane biodegradation in stirred tank bioreactors.

机构信息

Departamento de Procesos y Tecnología, Universidad Autónoma Metropolitana-Unidad Cuajimalpa, Avenida Vasco de Quiroga 4871, Col. Santa Fe Cuajimalpa. Delegación Cuajimalpa de Morelos, Ciudad de México, Mexico; Department of Chemical Engineering and Environmental Technology, School of Industrial Engineering, University of Valladolid, Dr. Mergelina, s/n, 47011, Valladolid, Spain.

Departamento de Procesos y Tecnología, Universidad Autónoma Metropolitana-Unidad Cuajimalpa, Avenida Vasco de Quiroga 4871, Col. Santa Fe Cuajimalpa. Delegación Cuajimalpa de Morelos, Ciudad de México, Mexico.

出版信息

J Environ Manage. 2018 Jul 1;217:247-252. doi: 10.1016/j.jenvman.2018.03.097. Epub 2018 Apr 5.

DOI:10.1016/j.jenvman.2018.03.097
PMID:29605779
Abstract

This study aimed at systematically comparing the potential of two empirical methods for the estimation of the volumetric CH mass transfer coefficient (ka), namely gassing-out and oxygen transfer rate (OTR), to describe CH biodegradation in a fermenter operated with a methanotrophic consortium at 400, 600 and 800 rpm. The ka estimated from the OTR methodology accurately predicted the CH elimination capacity (EC) under CH mass transfer limiting conditions regardless of the stirring rate (∼9% of average error between empirical and estimated ECs). Thus, empirical CH-ECs of 37.8 ± 5.8, 42.5 ± 5.4 and 62.3 ± 5.2 g CH m hvs predicted CH-ECs of 35.6 ± 2.2, 50.1 ± 2.3 and 59.6 ± 3.4 g CH m h were recorded at 400, 600 and 800 rpm, respectively. The rapid Co-catalyzed reaction of O with SO in the vicinity of the gas-liquid interphase during OTR determinations, mimicking microbial CH uptake in the biotic experiments, was central to accurately describe the ka.

摘要

本研究旨在系统比较两种经验方法(鼓泡法和氧转移速率法)估算体积 CH 传质系数(ka)的潜力,以描述在 400、600 和 800 rpm 下以甲烷氧化菌共生物为基础的发酵罐中 CH 生物降解的情况。OTR 方法估算的 ka 能够准确预测 CH 消除容量(EC),即使在 CH 传质受限条件下,也不受搅拌速率的影响(经验和估计的 EC 之间的平均误差约为 9%)。因此,在 400、600 和 800 rpm 下,分别记录到的 37.8±5.8、42.5±5.4 和 62.3±5.2 g CH m hvs 的经验性 CH-ECs,预测的 CH-ECs 为 35.6±2.2、50.1±2.3 和 59.6±3.4 g CH m h。在 OTR 测定过程中,SO 在气液界面附近与 O 的快速协催化反应模拟了生物实验中微生物对 CH 的吸收,这对准确描述 ka 至关重要。

相似文献

1
A systematic comparison of two empirical gas-liquid mass transfer determination methodologies to characterize methane biodegradation in stirred tank bioreactors.两种经验性气液传质测定方法在搅拌罐生物反应器中表征甲烷生物降解的系统比较。
J Environ Manage. 2018 Jul 1;217:247-252. doi: 10.1016/j.jenvman.2018.03.097. Epub 2018 Apr 5.
2
Oxidation of methane in biotrickling filters inoculated with methanotrophic bacteria.接种甲烷氧化菌的生物滴滤塔中甲烷的氧化。
Environ Sci Pollut Res Int. 2017 Nov;24(33):25702-25712. doi: 10.1007/s11356-016-7133-z. Epub 2016 Jul 1.
3
Bioreactor scale-up and oxygen transfer rate in microbial processes: an overview.微生物过程中的生物反应器放大与氧传递速率:综述
Biotechnol Adv. 2009 Mar-Apr;27(2):153-76. doi: 10.1016/j.biotechadv.2008.10.006. Epub 2008 Nov 12.
4
Comparative performance evaluation of conventional and two-phase hydrophobic stirred tank reactors for methane abatement: Mass transfer and biological considerations.
Biotechnol Bioeng. 2016 Jun;113(6):1203-12. doi: 10.1002/bit.25897. Epub 2015 Dec 10.
5
Assessing the influence of CH4 concentration during culture enrichment on the biodegradation kinetics and population structure.评估培养富集过程中CH4浓度对生物降解动力学和种群结构的影响。
J Environ Manage. 2014 Dec 15;146:116-123. doi: 10.1016/j.jenvman.2014.06.026. Epub 2014 Aug 27.
6
Methane-dependent denitrification by a semi-partitioned reactor supplied separately with methane and oxygen.通过分别供应甲烷和氧气的半分隔式反应器进行依赖甲烷的反硝化作用。
Bioresour Technol. 2005 May;96(8):921-7. doi: 10.1016/j.biortech.2004.08.016. Epub 2004 Nov 11.
7
Gaseous hexane biodegradation by Fusarium solani in two liquid phase packed-bed and stirred-tank bioreactors.茄病镰刀菌在两个液相填充床和搅拌罐生物反应器中对气态己烷的生物降解作用
Environ Sci Technol. 2006 Apr 1;40(7):2390-5. doi: 10.1021/es051512m.
8
Biogas valorization via continuous polyhydroxybutyrate production by Methylocystis hirsuta in a bubble column bioreactor.利用泡状柱生物反应器中的 Methylocystis hirsuta 连续生产聚羟基丁酸酯来实现沼气增值。
Waste Manag. 2020 Jul 15;113:395-403. doi: 10.1016/j.wasman.2020.06.009. Epub 2020 Jun 22.
9
Methanotrophic activity in a diffusive methane/oxygen counter-gradient in an unsaturated porous medium.不饱和多孔介质中扩散性甲烷/氧气逆向梯度下的甲烷营养活性。
J Contam Hydrol. 2007 Oct 30;94(1-2):126-38. doi: 10.1016/j.jconhyd.2007.05.006. Epub 2007 Jun 12.
10
Evaluation of the influence of methane and copper concentration and methane mass transport on the community structure and biodegradation kinetics of methanotrophic cultures.
J Environ Manage. 2016 Apr 15;171:11-20. doi: 10.1016/j.jenvman.2016.02.002. Epub 2016 Feb 8.

引用本文的文献

1
Ectoine Production from Biogas in Waste Treatment Facilities: A Techno-Economic and Sensitivity Analysis.废弃物处理设施中利用沼气生产四氢嘧啶:技术经济与敏感性分析
ACS Sustain Chem Eng. 2021 Dec 27;9(51):17371-17380. doi: 10.1021/acssuschemeng.1c06772. Epub 2021 Dec 15.